Processs to obtain random terpolymers derived from itaconic acid, aconitic acid and/or its isomers, and alkenyl sulfonates and use of the product thereof

ABSTRACT

Random terpolymers are characterized for being tolerant to high concentrations of divalent ions, such as calcium, magnesium, strontium and barium, and that for their application in the reservoir or production rig, treated water, sea water and/or connate water can be used as means of transportation. Furthermore, the terpolymer also can be used to inhibit and disperse mineral scales presents in cooling system and boiler employed in the chemical and oil industry.Also, random terpolymers of the present invention have the characteristic of complying with environmental standards established internationally and are classified as particularly non-toxic, so it can be used in pipes and equipment of the petrochemical industry and with the use characteristic freshwater and seawater from offshore and onshore facilities.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. patent application Ser. No.15/129,245, filed Sep. 26, 2016, which is a national stage entry under35 U.S.C. of 371 of PCT Patent Application No. PCT/MX2015/000042, filedMar. 13, 2015, which claims priority to Mexican Patent Application No.MX/A/2014003577, filed Mar. 25, 2014, the entire contents of each ofwhich are incorporated herein by reference.

DESCRIPTION Technical Field of the Invention

The present invention is related to the process for obtaining randomterpolymers derived from itaconic acid, aconitic acid and/or itsisomers, and sodium alkenyl sulfonates through a free radicalpolymerization at an acid pH involving a redox system as initiator andtheir use in the inhibition of mineral scales like calcium carbonate,sulphates of calcium, strontium and barium, likewise dispersing ofcalcium carbonate, sulfate calcium, iron oxides and clays are alsoshown. The random terpolymers prevent and control de formation damageand rig production obstruction in the hydrocarbon extractive industry,which are caused by mineral salt deposits present in oilfields due thehigh salinity of formation water, pressure, temperatures and pH changes.Random terpolymers are used to inhibit and disperse mineral scalespresent in cooling systems and industrial boilers used in the oil andchemical industry. Likewise are characterized by being tolerant to highconcentrations of divalent ions, such as calcium, magnesium, strontiumand barium. In other hand for application in the field or on theproduction rig, treated water can be used as a means of transport likesea water or feature water from the site. Moreover, terpolymers of thepresent invention containing low toxicity are being employed under hightemperature.

Background of the Invention

The formation of scales in areas possessing low (matrix) and high(fractures) conductivity of oilfields, as well as systems oil drilling,production systems, surface equipment, boilers and cooling systemsgreatly contributes in the presented problems in petroleum operations.

The most mineral scales found in the oil fields are formed byprecipitation of ions present in the formation water as mineral phases,or well as a result of produced water which becomes supersaturated inmineral components when two types of streams, are incompatible and incontact (water-injection formation water), in the bottom of the well orin the rock formation. Whenever that a well is producing water, or usinginjection water as a method of recovery, arises the possibility thatmineral scale formation take place.

The formation damage is defined as the partial or total blockage derivedfrom natural or induced conditions presented in the rock to fluid flowfrom the producing formation (oil and gas) into the well or vice versa,is a problem that can occur in the different stages of the oil recoveryand production operations as a result of a change in the most importantpetrophysical properties of the rock such as the effective porosity andabsolute permeability. The formation damage can occur naturally or dueto induced conditions by the employed fluids in the operations carriedout in wells, such as drilling, cementing, completion, repair,production stimulation treatment and water injection or gas.

Mineral scales can be developed in the pores of the formation near tothe well, thus, the porosity and permeability of the rock lookdrastically reduced and can also be present in the production andinjection tubing, the facts mentioned above have as consequence:formation damage from the oil reservoir, decreased production of crudeoil, restriction problems with the water injection flow (pressurelosses), workover of wells due to the reduction in production, corrosionin production and injection pipes and surface equipment, among others.All these problems lead to costly cleaning treatments, in addition tothe replacement and maintenance of equipment and pipelines, likewise ifthis situation is not adequately controlled will occur the loss of aproduction well.

The main factors influencing the formation of these deposits are:temperature, pressure, flow rate, salinity, concentration of dissolvedsolids in water, pH, and others.

The mineral deposits found in areas of low (matrix) and highconductivity (fractures) into the oil reservoir are different incomposition, these mainly are composed of calcium carbonate, calcium,strontium and barium sulfate, as well as iron oxides in proportions thatdepend of the thermodynamic conditions present in the aqueous system.

Some mineral scales, such as calcium carbonate (CaCO₃), can be dissolvedwith acid medium, but this fact depends importantly on the purity of themineral, because generally calcium carbonate is combined with otherminerals such as calcium sulfate and barium sulfate, which are verystable in acidic environments.

The contained brines in oil reservoirs have particles such as clays, andprecipitates, mainly calcium compounds. The particles can be depositedand may be grown up on the surfaces, producing excessive sediment inareas possessing low water velocity, and interfering with the flow ofwater through the effective porosity of the oil reservoir.

For the particular case of the ancillary services area, the formation ofdeposits in cooling systems is one of the most important problems forthe production operations in the industry. The main problems that causemineral scale deposits are decreased heat transfer, flow restriction(pressure losses), corrosion, among others, which leads to the highcleaning costs, the replacement and maintenance of equipment andpipeline.

In worldwide to counter such problems, have been used several methods,in which stand for its efficiency and cost, chemical additives such asscale inhibitors, dispersants of inorganic salts and solvents acidseither in together or independently.

Among the most common used chemicals are:

1) Sequestering agents. They function by chelation of cations (Ca2+,Ba2+, Sr2+) present in the connate water so that their solubilityproducts are not exceeded due to the concentration. One of the most usedproducts is ethylene diamine tetra acetic acid (EDTA). The disadvantagesof these products are:

-   -   a) Because these operating in stoichiometric form, a large        amount of chelating agent is required, and this is undesirable        from the economic viewpoint.    -   b) These are effective only at low concentrations of dissolved        divalent ions.

2) Poly (phosphates). The most used are sodium hexametaphosphate (NaPO3)6, sodium tripolyphosphate (Na₅P₃O₁₀) and various oligo-phosphates, suchas those indicated in U.S. Pat. No. 2,358,222 wherein the structuralformulas are: Na₉P₇O₂₂, Na₄P₂O₇, Na₆P₄O₁₃, Na₅P₃O₁₀. These inhibitorsfunction in water containing moderate concentrations of calcium and nearto neutral pH. The problem with poly (phosphates) is that thephosphorus-oxygen bond (PO) is often reduced and the orthophosphate ionis formed (PO₄ ⁻³) (J. Phys. Chem. A 1998, 102, 2838-2841), which canreact with calcium ions (Ca²⁺) to form calcium phosphate [CaHPO₄ and Ca₃(PO₄)₂]. It has been reported in the literature (U.S. Pat. No. 4,673,508“Inhibition of calcium phosphate scale formation with a maleate polymer”EP0267597A2 “Calcium phosphonate inhibition”, U.S. Pat. No. 4,929,632“Calcium phosphate scale methods control”), that such compounds generateproblems as blockage in pipes, corrosion and decrease in heat transferequipment when high concentrations of divalent ions, high temperatureand extreme changes in pH.

3) Organophosphonates. These are compounds containing in their structurethe carbon-phosphorus bond (P—C), which function through inhibitionmechanism at the threshold of precipitation and the crystalmodification. Organophosphonates are widely used as scale inhibitors ofcalcium carbonate. Among the most common are (1): 1-hydroxyethylene 1,1diphosphonic acid (a), amino acid tri-methylene phosphonic (b) andphosphonic pentamethylene acid diethylenetriamine (c).

-   -   Phosphate used as scale inhibitors a) ethylene 1-hydroxy        1,1-diphosphonic acid, b) tri-methylene phosphonic amino        acid, c) pentamethylene phosphonic diethylene triamine acid.

Besides there are other organophosphates having application asantiscaling as is indicated in the following patent documents:

The U.S. Pat. No. 3,974,090 pointed the synthesis and use ofphosphonates having the structural formula shown below:

The U.S. Pat. No. 3,886,205 described and protected the synthesis anduse of a scale inhibitor compound which is shown below:

The mentioned inhibitors above have the advantage that thephosphorus-carbon bond is less susceptible to hydrolysis, but undersevere operating conditions such as sudden changes in pH, highconcentration of calcium ion and temperatures above 150° C. causes thatthese are capable to react with calcium ions to form calcium phosphates(G. E. Geiger, Water & Process Technology, 2006, 1-7, “NewNon-Phosphorous Calcium Carbonate Inhibitor Reduces Phosphorus Levelsand Overcomes Limitations of Phosphonates”; Ruenradee Prachasri,“Developing a New Environmentally Acceptable Non-Phosphorus CoolingWater Treatment Program”, Electricity Generating Authority of Thailand,Nonthaburi 11130, Thailand; W. Wang, A. T. Kan, M. B. Tomson, SPE155108, 2012, 1-16; “A Novel and Comprehensive Study and Polymeric andTraditional Phosphonate inhibitors for High Temperature Scale Control”;F. H. Browning, H. S. Fogler, Langmuir 1995, 11, 4143-52; “Effect ofsynthesis parameters on the properties of calcium phosphonateprecipitates”). In Complementary way, organophosphates are susceptibleto severe degradation by oxidizing biocides (Separation Science andTechnology, 42, 2007, 1639-1649; “Degradation of Phosphonate-Based ScaleInhibitor Additives in the Presence of Oxidizing Biocides: “CollateralDamages” in Industrial Water Systems”) and to form orthophosphate ionswhich can react with calcium ions present in the water and after resultin calcium phosphates forms and therefore generating pipe obstructionproblems and decreased heat transfer in cooling systems. Polymers.Polymeric anti scaling generally inhibit the mineral phases formation bythe chemisorption on the faces of the active sites from themicrocrystals, and by phenomena such as crystalline modification,dispersion, the inhibition in the threshold of precipitation andpreventing growth and agglomeration of microcrystals.

Some of the most used polymers (4) are sodium poly (acrylate), sodiumpoly (maleic acid), sodium polyvinyl sulfonate and copolymers derivedfrom acrylic acid-sodium vinyl sulfonate.

Polymers used as scale inhibitors: a) sodium poly (acrylate), b) poly(maleic acid), c) sodium polyvinyl sulfonate and d) copolymer derivativefrom acrylic acid-sodium vinyl sulfonate.

Also, in order to create improved systems it has been developed somecompositions containing various anti scaling agents among which are thefollowing:

The MX/a/2013/004644 Mexican request patent (“Process to obtain randomcopolymers derived of itaconic acid and/or its isomers and alkenylsulphonates and use of the obtained product”), described the process ofobtaining random copolymers itaconic acid derivatives and/or isomersthereof and alkenyl sulphonates and their use as inhibitors/dispersantsof mineral scale as calcium carbonate and calcium sulphates, barium andstrontium sulphates for petroleum oil reservoirs and in the service areaas the cooling systems and boilers used in the chemical and oilindustry.

EP 0256057B1 European Request Patent (“Scale Inhibitor”) described theuse of chemical products to prevent the formation of calcium andmagnesium scales in evaporation systems, boilers and water purificationequipment. This patent focuses on the synergistic effect when threeinhibitors are combined. The evaluations were performed using differentcombinations of scale inhibitors in the way to find the most effectiveformulation for control CaSO₃, CaCO₃ and Mg(OH)₂ scales. The mosteffective formulation consisted of two polymers (maleic polyacid andcopolymer derived from styrene sulfonate and maleic acid) and also aminophosphonic acid. U.S. Pat. No. 4,065,607 (“terpolymers of maleicanhydride and their use as scale control agents”). Described a newprocess for obtaining a derived terpolymer from maleic anhydride,acrylamide or methacrylamide and a third monomer compound of styrene oroctene, this process uses a mixture of aromatic solvents and ketones ata temperature of 120° C. The terpolymers are useful in inhibitingcalcium carbonate scale.

The EP0976911A1 European Request Patent (“Scale inhibitors”). Describeda composition of commercial scale inhibitors used in extraction systemsand production of hydrocarbons. The compositions contained commercialinhibitors, such as phosphonates, copolymers and based terpolymers inacid acrylic, acid phosphino-carboxylate and combined with aminesphosphate esters inhibitors, since this combination provided anadvantage over conventional inhibitors especially used diethylenetriamine tetrametilenfosfato. Amines of this type have thecharacteristic of remaining in the fluid in a wide temperature range aswell as being soluble in hydrocarbons such as kerosene, diesel and heavyaromatic naphthas.

The U.S. Pat. No. 4,331,792 (“Continuous process for production ofcopolymer of an alkali metal vinyl sulfonate and acrylic acid”),described the continuous production process of the based copolymer invinyl sulfonate and acrylic acid, in which the monomers are mixed andthe pH adjusted to a range of 4-5.5. Furthermore, the reaction medium iscombined with ammonium persulfate and sodium bisulfite as catalyticagents that promote free radical. The reaction is carried out in atubular reactor adiabatically operated at temperatures of 140-220° C.and residence times of 5 to 7 minutes, while the resulting copolymer isremoved by precipitation with methanol. Also, the patent mentioned thatthe obtained copolymer is useful for preventing the scales formation ofcalcium and magnesium.

The U.S. Pat. No. 4,710,303 (“Low molecular weight polyvinyl sulfonatefor low pH barium sulfate scale control”), described a method forinhibiting the scaling with polyvinyl sulfonate and compared theireffectiveness with respect to other compounds (phosphate esters, sodiumhexametaphosphate, 1-hydroxyethylene-1,1-ácidodifosfonico,diethylenetriamine phosphonate, acrylic-acid copolymer maleic acid,polyacrylic acid) in a synthetic brine containing Ba²+ and SO₄ ²⁻ ions.Based on this method, is accurate that sodium polyvinyl sulfonate iseffective in inhibiting of scales to pH=2.5-4 conditions and atemperature of 70° C. in 5-10 ppm as concentration.

The U.S. Pat. No. 5,089,150 (“Method of Increasing retention of scaleinhibitors in subterranean formations”) disclosed a method forcrosslinking polymers acrylates base and phosphates polymer hydroxideslike base make more resistant and compatible compounds in high salinityenvironments characteristic of underground formations. According to thispatent, the key point in the stability of the inhibitors is incrosslinking polymers with polyols, which occurs by esterification ofthe carboxylate inhibitor and hydroxides polyalcohol, which causes toincrease the molecular weight of the polymer chains, and similarly, ifthe polymer consists of phosphate groups. As test method they used Bereaas clay rock type pre-saturated with connate water at 90° C. andinjected with 2000 ppm of dissolved inhibitor in seawater per 15 percentpore volume.

The U.S. Pat. No. 8,215,398 (“Polysaccharide based scale inhibitor”),proposed a method for modifying polysaccharides, due to that derivativesfrom these compounds are found to be effective in inhibiting differenttypes of deposits. The modified polysaccharide has a molecular weight ofup to 500,000 AMU, also has the characteristic of being biodegradableand resistant to high temperatures. Usually is employed in the corrosioncontrol and the mineral deposits due to its high tolerance to organicand inorganic salts such as chlorides of sodium, potassium and calciumand magnesium ions.

The 2002/0150499A1 US patent (“Oil-soluble scale inhibitors withimproved formulation for environmental classification”) presentedinformation about the composition of scale inhibitors with applicationin hydrocarbon production systems. The formulations contained commercialinhibitors in its acid form, 2-ethyl-hexylamine (2-EHA) and the likeamines. The formulations described have the advantage over conventionalscale inhibitors, because they are less toxic and biodegradable.

The 2005/0282712A1 US patent (“Scale Control composition for highscaling environments”) described the effectiveness of phosphonatespolymers, sulfonate sodium base and unsaturated dicarboxylates, whichare useful in scale control of BaSO₄ and CaCO₃ in oilfield formations.

The 2007/0267193A1 US patent (“Stimulating oilfields using differentscale-inhibitors”) disclosed a method for stimulating a reservoir, usingscale inhibitors, with secondary recovery techniques. The methodcomprises injecting steam and measuring inhibitor fractions contained inthe recovered fluids.

The 2010/0163494A1 US patent (“Preparation of environmentally acceptablescale inhibitors”) disclosed a method for scale control using aminoacids for preparing alkyl phosphonates, which are obtained bycontrolling the reaction of alkyl phosphonation. According to thisproposal, hydrogens to be replaced (H) of each group with alkylphosphonate amine groups (—R—PO—(OH)₂) these compounds are veryeffective in inhibiting inlays CaCO₃ and BaSO₄. However, the monoalkylated amino acids tend to be more biodegradable than thedi-substituted alkyl-phosphonates amino acids.

The U.S. Pat. No. 6,924,253 B2 (“Scale removal”) disclosed a method toremove scales (mainly CaCO₃ and BaSO₄) inside or near the productionwell in oil recovery processes using ionic liquids as1-ethyl-3-tetrachloroaluminate methylimidazole, 1-butilpiridin nitrate,1-ethyl-3-methyl imidazole tetrafluoroborate and 1-butilpiridinohexafluorophosphate.

The U.S. Pat. No. 6,995,120 (“Scale Control composition for high scalingenvironment) protected an inhibitory composition of calcium carbonateand/or barium sulfate scales composed of a water-soluble polymer havingincorporated functionality phosphate, the polymer is formed of at leastone monomer of unsaturated carboxylic acid ethylenically, at least onemonomer of unsaturated vinyl sulfonate ethylenically, or a mixturethereof. Within the patent specifically is protected the terpolymerderived from the polymerization process of acrylic acid with2-acrylamido 2-methyl propane sulfonic phosphate ester and oleylethoxylate.

The U.S. Pat. No. 5,282,976 (“terpolymer useful as a scale inhibitor”)protected the synthesis and application as soluble antiscaling agent inwater a new terpolymer derived from the polymerization process monomersof acrylic acid or methacrylic acid, vinyl acetate vinyl alcohol andsodium 1-aliloxy-2-hydroxypropyl sulfonate.

The U.S. Pat. No. 4,952,327 (“Scale Control with terpolymers containingstyrene sulfonic acid”) described that the scale inhibition is obtainedby adding to an aqueous medium of 0.5 to 500 ppm from a copolymercontaining at least one of the following three monomers: a) carboxylicacids mono unsaturated as well as their salts and anhydrides, acidscontaining 3 to 5 carbon atoms, such as acrylic acid, methacrylic acidmaleic acid or anhydrides thereof; b) acrylamidoalkane sulfonic acidsand salts thereof, such as 2-acrylamido-2-methylpropane sulfonic acidand c) styrene sulfonic acid and its salts.

The U.S. Pat. No. 4,889,637 (“Scale Control with terpolymers containercontaining vinyl Alcohol”) described that the scale inhibition isobtained by adding to an aqueous medium of 0.5 to 500 ppm from acopolymer containing at least one of the following three monomers: a)carboxylic acids mono unsaturated as well as their salts and anhydrides,acids containing 3 to 5 carbon atoms, such as acrylic acid, methacrylicacid maleic acid or anhydrides thereof; b) acrylamidoalkane sulfonicacids and salts thereof, such as 2-acrylamido-2-methylpropane sulfonicacid and c) vinyl alcohol.

The U.S. Pat. No. 7,306,035 (“Process for treating a formation”)proposed a method to increase the production of the oil reservoirsemploying chemicals in the form of gels so that these, once within theformation, it encapsulated oil and facilitated their extraction.Moreover, this proposal took into account aspects such as the importanceof scales control, so proposed the use of other substances as additivesin the formulation of such gels.

The EP 1639228B1 European Patent (“Method for stimulating an oilfieldComprising using different scale-inhibitors”) described the increasedoil production by injecting water steam into the producing zone as adisplacement fluid and to recover it as a compounded fluid from oil, theintent of this proposal is to make injections of fluids in differentsegments of the producing zone. Also contemplated the use of scaleinhibitors at different concentrations and injected directly and/ordiluted.

Generally, this is a production method of oil in which the injectedinhibitor in different areas where improvements in the scale control isallowed.

Under the demands of the oil production processes, as well as in thearea of services, specifically cooling systems and boilers, thesesubstances must be able to work in severe operating conditions and havelow toxicity.

Therefore, the development of improved mineral scales inhibitors anddispersants is a worldwide objective which is continually pursued, andis the object of the present invention.

We mention that the supramolecular chemistry is the part of thechemistry to study of systems involving aggregates of molecules or ionsthat are joined through non-covalent bonds, such as electrostaticinteractions, coordination bonds, and hydrogen bonding interactions, π-πinteractions, dispersion interactions and solvent effects.

Since the energy standpoint, the supramolecular interactions are weakerthan covalent bonds, which are located in the energy range of 150 to 450kJ/mol for single bonds. The energy range of noncovalent interactions islocated from 2 kj/mol for dispersion interactions to 300 kJ/mol forion-ion interactions (Table 1) and the sum of several supramolecularinteractions can give rise to highly stable supramolecular complexes.

TABLE 1 Strength of supramolecular interactions Interactions Strength(Kj/mol) Ion-ion 200-300 Ion-dipole  50-200 Dipole-dipole  5-50 Hydrogenbridge  4-120 Cation- 

 5-80

 - 

 0-50 Van der Walls <5 Hydrophobic The related energy with thesolvent-solvent interaction

As for the formation of supramolecular complexes from the interaction ofpolymers or organic compounds with mineral salts possessing scalingproperties, in literature are found the following examples:

The titled article “Binding of Calcium Carbonate and to Polyacrylates”(Journal of Physical Chemistry B 2009, 113, 7081-7085) suggested thatthe interaction of polyacrylates with calcium carbonate is athermodynamically favored process that gives rise to the formation ofcomplexes, which have the characteristic of preventing the crystalgrowth of calcium carbonate.

The titled article “Control of Crystal Nucleation and Growth of CalciumCarbonate by Synthetic Substrates” (Chemistry of Materials 2001, 13,3245-3259) indicated that the nucleation and growth of calcium carbonatecrystals may be controlled through the use of synthetic substrates andthat in such process took place the supramolecular complexes formationderived from the adsorption process of monomers or carboxylated polymerson surfaces of calcium carbonate.

The article entitled “A New Design Strategy for Molecular Recognition inheterogeneous Systems: A Universal Crystal-Face Growth Inhibitors forBarium Sulfate”, Peter V. et al. (J. Am. Chem. Soc. 2000, 122,11557-11558) indicated that the design strategy of new additives tocontrol scaling problems are based on the molecular recognition and thatderived macrocycles from poly-aminometilfosfonatos controlled the growthin barium sulfate crystals through the complex formation.

The titled article “At the interface of Organic Chemistry and Inorganic:Bioinspired Synthesis of Composite Materials (Chemistry of Materials2001, 13, 3227-3235)” indicated that the design of artificial modelsfrom biomineralization processes has let that research was binded ininorganic materials and supramolecular chemistry and that polyamideswith carboxylate ligands can interacting with calcite crystals. Also, inthe article it mentioned that block copolymers with two hydrophilicgroups have been successfully used for modulating the morphology ofinorganic materials such as calcium carbonate and barium sulfate.

The Computational chemistry is a tool widely used at worldwide topredict the stability and structure of chemical systems with improvedand potential properties and has found application at industrial levelin the development of studies about quantitative structure-activityrelationship. Within the computational methods that has been employedfor this purpose are presented the molecular mechanics methods, quantummethods, within which are semiempirical, ab initio and Densityfunctional theory methods. As examples in the literature is demonstratedthe use of computational chemistry to predict accurately supramolecularinteractions in chemical systems, thermodynamic aspects and kineticfeatures of chemical processes which may be mentioned in entitledarticles: 1) Cornucopian Aggregate Cylindrical morphologies fromSelf-Triblock Copolymer of Amphiphilic assembly in Selective Media(Journal of Physical Chemistry B, 2005, 109, 21549-21555), 2) DensityFunctional Calculations, Synthesis, and Characterization of Two NovelQuadruple Hydrogen-Bonded Supramolecular Complexes (Journal of PhysicalChemistry A, 2004, 108, 5258-5267), 3) Strong Decrease of theBenzene-Ammonium Ion Complexation upon Interaction with a CarboxylateAnion (Journal of the American Chemical Society, 1999, 121, 2303-2306).

Is important to point that in anyone of the above references does notdiscuss the obtaining of random terpolymers derivatived of itaconic acidand aconitic acid, and/or isomers and alkenyl sulphonates and their usein inhibiting mineral scale as calcium carbonate and sulphates barium,strontium and calcium presented by the incompatibility of water (waterof injection and formation) in an oil field, as well as in the rigproduction from an oil well and as dispersing of clay, calciumcarbonate, sulphate of barium, strontium and calcium and iron oxidespresented in oil installations. The use in cooling systems and boilerspresent in the oil and chemical industry also it does not mention.

BRIEF DESCRIPTION OF THE DRAWINGS OF THE INVENTION

In order to have a better understanding as to the application ofterpolymers as inhibitors and dispersants of mineral scale of thepresent invention, in the following step will be referenced to thedrawings made and described below:

In the FIG. 1 the infrared spectrum of the product 1 is shown.

In the FIG. 2 ¹H Resonance Magnetical Nuclear (RMN) of the product 1 isshown.

In the FIG. 3 ¹³C Resonance Magnetical Nuclear (RMN) del producto 1 isshown.

In the FIG. 4 morphology and composition of calcium sulfate crystals areshown, a) without chemical and b) 200 ppm of product 1.

In the FIG. 5 morphology and composition of calcium carbonate crystalsare shown, a) without chemical and b) 200 ppm of product 1.

In the FIG. 6 the operation basis of a photometer are shown In FIG. 7 achemical structure A representing a random terpolymer based on itaconicacid, sodium vinyl sulfonate and aconitic acid with molecular weight of903 AMU and polydispersity index of 1 is shown.

In FIG. 8 a surface B chemical structure representing calcium carbonatecrystals in their calcite polymorphic form is shown.

In FIG. 9 a supramolecular complex C obtained using computationalchemistry and after the compound A surface B interaction process isshown.

In FIG. 10 a supramolecular complex C formation from compound A andsurface D molecular interaction is shown.

In FIG. 11 a chemical structure of surface D representing barium sulfatecrystals in its polymorphic form of barite is shown.

In FIG. 12 a supramolecular complex E obtained using computationalchemistry after compound A with surface F interaction process is shown.

In FIG. 13 a supramolecular complex E formation from compound A andsurface D molecular interaction is shown.

In FIG. 14 a chemical structure of the F surface representing crystalsof calcium sulfate in its polymorphic form of anhydrite is shown.

In FIG. 15 a supramolecular complex G obtained using computationalchemistry after compound A with surface F interaction process is shown.

In FIG. 16 a supramolecular complex G formation from compound A andsurface F molecular interaction is shown.

DETAILED DESCRIPTION OF THE INVENTION

The present invention is related to the process of obtaining randomterpolymers based on itaconic acid or its isomers, aconitic acid ortheir isomers and sodium alkenyl sulphonates of structural formula (5),through a polymerization in aqueous solution via free radicals at acidpH in the range of 1.0 to 3.5 and as initiator a redox system, and theiruse as inhibitors of mineral scale such as calcium carbonate, calciumsulphate, strontium and barium, and clay dispersing, iron oxides,carbonate and calcium sulfate.

The terpolymers prevent and control the formation damage and obstructionby hydrocarbons in production rigs, which are caused by mineral saltdeposits present in oilfields and whose origin is the contained highsalinity in formation water, incompatible mixtures of water injectionand formation water, pressure changes, temperature and pH.

The terpolymers are used to inhibit and disperse presented mineralscales in cooling systems and boilers employed in the oil and chemicalindustry and are characterized by being tolerant to high concentrationsof divalent ions, such as calcium, magnesium, strontium and barium ionsand for the application in the field or in production rig, treatedwater, sea water and/or feature water from the site is used as atransport medium. The random terpolymers of the present invention havethe characteristic of being used under high temperature, high salinityand have low toxicity.

Where: R₁=—H, —CH₃, R₂=—H, —CH₂COOH, —COOH, R₃=—COOH, R₄=—CH₂COOH, H,R₅=—H, R₆=—H, R₇=—H, —CH₃, R₈=—SO₃Na, —CH₂SO₃Na, —CONHC(CH₃)₂CH₂SO₃Na,C₆H₄SO₃Na, R₉=H, R₁₀=—COOH, R₁₁=—COOH, R₁₂=—CH₂COOH and n is between 2and 70.

For the development of the present invention a method comprising thefollowing steps was followed: 1) molecular design through computationalchemistry, 2) Synthesis and characterization of random terpolymers and3) experimental evaluation of anti-scaling and dispersant properties

The selection of this methodology is based on the fact that the key todevelop agents tolerant anti-scaling at high salinities andconcentrations of divalent ions and able to withstand conditions of hightemperatures and pressures is the understanding at the molecular levelof as random terpolymers based on itaconic acid or isomers thereof,aconitic acid or their isomers and sodium alkenyl sulphonates areadsorbed on mineral salt crystals with anti-scaling properties and giverise to the supramolecular complex formation capable of:

1) Inhibiting on the threshold of precipitation just after a nucleationcenter is formed. The terpolymer will be adsorbed in one of the facesfrom the microcrystalline nucleation center in the inorganic salt andthe formed ion pair will prevent the diffusion of ions to the growthcenters; 2) To distort or alter the crystal lattice. If the terpolymeris adsorbed on a crystal from an inorganic salt, alterations will beoccurred in the surface properties such as size, adhesion, hardness,toughness, crystal structure, etc.; consequently resulting in fragmentedcrystals, become amorphous, soft and slightly sticky, and thereforefacilitate its removal by the continuous flow of water and 3) Todisperse. Sulfonates functional groups and di-carboxylic acids of theterpolymers will be adsorbed on the active sites of the growing crystalsand through the polymer chains, repulsion effects, will be generated sosteric and electrostatic which will increase the colloidal stability ofthe inorganic particles to keep them dispersed and avoid itsagglomeration, so its removal will be provided through the continuousflow of water.

Nowadays before to develop new chemicals with improved properties, themolecule which seeks to solve a particular problem can be designedthrough theoretical studies of computational chemistry, according withthe following explanation:

-   -   a) The chemical structure from A compound shown in FIG. 7,        representing a random terpolymer based itaconic acid, sodium        vinyl sulfonate and aconitic acid with 903 AMU as molecular        weight and polydispersity index of 1 was used.    -   b) The chemical structure of the B surface shown in FIG. 8,        representing calcium carbonate crystals in its polymorphic form        of calcite was used.    -   c) The geometries of the chemical structure of A compound and        the B surface were minimized considering energy in a solvated        medium by water (dielectric constant 78.54) through quantum        chemical methods using Density Functional Theory and LDA-VW        Functional.    -   d) Through computational chemistry and using a water solvated        medium (dielectric constant 78.54) with quantum chemical methods        using Functional Theory Density and LDA-VW Functional, the        compound A was interacted with the surface B, resulting in the C        supramolecular complex formation shown in FIG. 9, and the energy        results that are shown in Table 2.    -   e) The analysis of the results in Table 2 shown that the        formation of C supramolecular complex from the molecular        interaction between the A compound and the B surface (9) is        strongly favored from the thermodynamic point of view. Also, the        interaction energy of −113.12 kcal/mol (−473.29 kJ/mol)        indicated that ion-ion supramolecular interactions are presented        so as well a combination of ion-dipole interactions and hydrogen        bonding type.

TABLE 2 Energy of Compound A, surface B and supramolecular complex Cobtained through quantum chemical methods using Density FunctionalTheory and LDA-VW Functional. Density Functional Theory, and LDA-VWFunctional Compounds Total Energy Interaction Energy or Complex(kcal/mol) (kcal/mol) A −2,641,697.44 B −70,629,855.35 C −73,271,665.91−113.12

Where:

A=Random terpolymer based on itaconic acid, sodium vinyl sulphonate andaconitic acid with molecular weight of 903 AMU and polydispersity indexof 1.

B=Calcium carbonate surface in theft polymorphic form of calcite.

C=Supramolecular complex derived from the interaction of the randomterpolymer based on itaconic acid, sodium vinyl sulfonate and aconiticacid with molecular weight of 903 AMU and polydispersity index of 1,corresponding to compound A, as shown in FIG. 7, and the surface ofcalcium carbonate in its polymorphic form calcite B, as shown in FIG. 8.

Determination of the Interaction Between Random Terpolymer Based onItaconic Acid, Sodium Vinyl Sulfonate and Aconitic Acid with BariumSulfate.

In order to determine the capacity that random terpolymers based onitaconic acid, sodium vinyl sulfonate and aconitic acid would have inorder to form supramolecular complexes with barium sulfate crystals andcontrol their growth, we proceeded to simulate through computationalchemistry and using a solvated medium by water (dielectric constant78.54) with quantum chemical methods using Density Functional Theory andthe LDA-VW functional, the process of interaction from a randomterpolymer based on itaconic acid, sodium vinyl sulfonate and aconiticacid, with 903 as molecular weight and polydispersity of 1,corresponding to the chemical structure of compound A, as shown in FIG.7, with the surface D that is shown in FIG. 11 and that representsbarium sulfate crystals in its polymorphic form of Barite, obtaining asresult the E supramolecular complex shown in FIG. 12, and the energyresults shown in Table 3.

The analysis of the results in Table 3 show that the E supramolecularcomplex formation shown in FIG. 13 from the molecular interaction of thecompound A and the D surface shown in FIGS. 6 and 11, respectively, isstrongly favored from the thermodynamic point of view. Also, theinteraction energy of −127.22 kcal/mol (−532.29 kJ/mol) indicated thatthese ion-ion supramolecular interactions and a combination ofion-dipole interactions and hydrogen bonds could be presented.

TABLE 3 Energy of compound A, Surface D and E supramolecular complexobtained through quantum chemical methods using Density FunctionalTheory and LDA-VW Functional. Density Functional Theory, and LDA-VWFunctional Compounds or Total Energy Interaction Energy Complex(kcal/mol) (kcal/mol) A −2,641,697.44 D −40,730,112.93 E −43,371,937.59−127.22

Where:

A=Random terpolymer based on itaconic acid, sodium vinyl sulphonate andaconitic acid with molecular weight of 903 AMU and polydispersity indexof 1.

D=Barium sulphate surface in their polymorphic form of baryta.

E=Supramolecular complex derived from the interaction of the randomterpolymer based on itaconic acid, sodium vinyl sulfonate and aconiticacid with molecular weight of 903 AMU and polydispersity of 1,corresponding to compound A (6), and the surface of barium sulphate inits polymorphic form of baryta B (7).

Determination of Interaction Between Random Terpolymer Based on ItaconicAcid, Sodium Vinyl Sulfonate and Aconitic Acid with Calcium Sulphate.

In order to determine the capacity that random terpolymers based onitaconic acid, vinyl sulfonate sodium and aconitic acid would have toform supramolecular complexes with crystals of calcium sulfate andcontrol their growth, in a first step it was proceeded to simulatethrough computational chemistry and using a solvated medium by water(dielectric constant 78.54) with quantum methods employing the DensityFunctional Theory and LDA-VW functional the process of interactionbetween a random terpolymer based on itaconic acid, sodium vinylsulfonate and aconitic acid, possessing 903 AMU as molecular weight andpolydispersity index of 1, corresponding to the chemical structure ofcompound A, as shown in FIG. 7, with the surface F shown in FIG. 14 andrepresenting crystals of calcium sulfate in its polymorphic form ofanhydrite, obtained as result shown in the supramolecular complex Gshown in FIG. 15, and the energy results that are shown in Table 4.

The analysis of the results presented in Table 4 show that the formationof G supramolecular complex, shown in FIG. 15, through the molecularinteraction between the A compound shown in FIG. 7 and the F surfaceshown in FIG. 14 would be strongly favored from the thermodynamic pointof view. Also, −136.14 kcal/mol (−569.61 kJ/mol) as the result ofinteraction energy indicated that supramolecular interactions of ion-iontype and a combination of ion-dipole interactions and hydrogen bondswould be presented.

The analysis of the results from the Tables 2 to 4 indicated that therandom terpolymers based on itaconic acid, sodium vinyl sulfonate andaconitic acid (6), objects of the present invention, have the ability toform supramolecular complexes with calcium carbonate crystals in itspolymorphic form of calcite, barium sulfate in its polymorphic form ofbarite and calcium sulfate in its polymorphic form of anhydrite; so aswell control the growth and morphology change thereof.

TABLE 4 Energy of compound A, Surface D and G supramolecular complexobtained through quantum chemical methods using Density FunctionalTheory and LDA-VW Functional. Density Functional Theory, and LDA-VWFunctional Compounds or Total Energy Interaction Energy Complex(kcal/mol) (kcal/mol) A −2,641,697.44 D −92,952,242.47 G −95,594,076.05−136.14

Where:

A=Random terpolymer based on itaconic acid, sodium vinyl sulphonate andaconitic acid with molecular weight of 903 AMU and polydispersity indexof 1.

D=Calcium sulphate surface in their polymorphic form of Anhydrite.

G=Supramolecular complex derived from the interaction of the randomterpolymer based on itaconic acid, sodium vinyl sulfonate and aconiticacid with molecular weight of 903 AMU and polydispersity index of 1,corresponding to compound A (6), and the surface of calcium sulphate inits polymorphic form of Anhydrite D (14).

Random Terpolymer synthesis and spectroscopic characterization. Therandom terpolymer based on itaconic acid, aconitic acid or its isomersand sodium vinyl sulfonate having the structural formula (5), object ofthe present invention are obtained by means of a polymerization processin aqueous solution via free radicals and a redox system as initiator.The polimerization is carried out at an acid pH in the range of 1.0 to3.5, under atmospheric pressure and at temperatures ranging from 50 to100° C. The obtained terpolymers are characterized for having a lowpolydispersity index ranging from 1 to 1.4 and low average molecularweights under 31,000 AMU.

EXAMPLES

The following examples will serve to illustrate the synthesis of therandom terpolymer based on itaconic acid, aconitic acid or its isomersand sodium vinyl sulfonate object of the present invention.

Example 1 (Product 1)

In a 1000 mL four-mouth round flask with a magnetic stirrer, acondenser, an addition funnel and a thermometer, 298 g of a solutioncontaining 25% by weight of sodium vinyl sulfonate, 60 g of itaconicacid and 100 g of aconitic acid are mixed at room temperature andatmospheric pressure. Afterwards, the reaction mixture is stirredvigorously and heated up to a temperature of 90° C. under atmosphericpressure in order to obtain a mixture with homogeneous and clearappearance. Once these conditions are attained, 1.24 g of ammoniumferric sulphate dodecahydrate are added and vigorous stirring ismaintained for 10 minutes. At a temperature of 90° C., 167 g of anaqueous solution containing 35% by weight of hydrogen peroxide is addedto the system. The reaction is exothermic so the temperature of thesystem was held at 92° C. (+/−2° C.). Once the addition process iscompleted, the reaction mixture is maintained under vigorous stirringand at a temperature of 92° C. (+/−2° C.), for 6 hours, time afterwhich, 640 g of a clear reddish liquid are obtained, which contains therandom terpolymer derived from itaconic acid, aconitic acid or itsisomers and sodium vinyl sulfonate referred to as product 1, with andaverage molecular weight of 984 AMU by number, an average molecularweight of 1090 AMU by weight and a polydispersity index of 1.11. Thesevalues were obtained by means of size exclusion chromatography (SEC)using a chromatography column with the trade name plaquagel MIXED-OH andan aqueous solution comprising sodium nitrate (0.2 M) and sodiumphosphate, monobasic (0.01 M) al a pH of 7 as the mobile phase.Spectroscopic characteristics are the following: FTIR (cm⁻¹): 3431,2942, 1714, 1402, 1155, 1036 y 724 (FIG. 1). ¹H NMR (D₂O), 200 MHz, δ(ppm): multiple signals at the 1.77 a 2.37, 2.38 a 3.25, 3.93 (FIG. 2).¹³C NMR (D₂O), 50 MHz, δ (ppm): signals at the 21.5 a 33.3, 37.5 a 46.5,50.5 a 65.7 y 174.3 a 177.1 (FIG. 3).

Example 2 (Product 2)

In a 1000 mL four mouth round flask supplied with a magnetic stirrer, acondenser an addition funnel and a thermometer, 298 g a solutioncontaining 25% by weight of sodium vinyl sulfonate, 149 g of itaconicacid and 100 g of aconitic acid are mixed at room temperature andatmospheric pressure. Afterwards, the reaction mixture is stirredvigorously and heated up to a temperature of 90° C. under atmosphericpressure in order to obtain a mixture with a homogeneous and clearappearance. Once these conditions are attained, 1.62 g of ammoniumferric sulphate dodecahydrate is added and vigorous stirring ismaintained for 10 minutes. At a temperature of 90° C., 167 g of anaqueous solution containing 35% by weight of hydrogen peroxide is addedto the system. The reaction is exothermic so the temperature of thesystem was held at 92° C. (+/−2° C.). The reaction is exothermic so thetemperature of the system was held at 92° C. (+/−2° C.). Once theaddition process is completed, the reaction mixture is maintained undervigorous stirring and at a temperature of 92° C. (+/−2° C.), for 6hours, time after which, 838 g of a clear reddish liquid are obtained,which contains the random terpolymer derived from itaconic acid,aconitic acid or its isomers and sodium vinyl sulfonate referred to asproduct 2, with and average molecular weight of 918 AMU by number, anaverage molecular weight of 1010 AMU by weight and a polydispersityindex of 1.11. These values were obtained by means of size exclusionchromatography (SEC) using a chromatography column with the trade nameplaquagel MIXED-OH and an aqueous solution comprising sodium nitrate(0.2 M) and sodium phosphate, monobasic (0.01 M) al a pH of 7 as themobile phase. Spectroscopic characteristics are the following: FTIR(cm⁻¹): 3431, 2939, 1713, 1407, 1154, 1036 y 71. ¹H NMR (D₂O), 200 MHz,δ (ppm): multiple signals at the 1.77 a 2.33, 2.72 a 3.02, 3.37 a 3.44.¹³C NMR (D20), 50 MHz, δ (ppm): signals at the 23.2 a 31.5, 39.9 a 43.6,49.1 a 58.5 y 176.9 a 181.4 intervals.

Example 3 (Product 3)

In a 1000 mL four mouth round flask supplied with a magnetic stirrer, acondenser an addition funnel and a thermometer, 298 g a solutioncontaining 25% by weight of sodium vinyl sulfonate, 37.3 g of itaconicacid and 100 g of aconitic acid are mixed at room temperature andatmospheric pressure. Afterwards, the reaction mixture is stirredvigorously and heated up to a temperature of 90° C. under atmosphericpressure in order to obtain a mixture with a homogeneous and clearappearance. Once these conditions are attained, 1.06 g of ammoniumferric sulphate dodecahydrate is added and vigorous stirring ismaintained for 10 minutes. At a temperature of 90° C., 142 g of anaqueous solution containing 35% by weight of hydrogen peroxide is addedto the system. The reaction is exothermic so the temperature of thesystem was held at 92° C. (+/−2° C.). Once the addition process iscompleted, the reaction mixture is maintained under vigorous stirringand at a temperature of 92° C. (+/−2° C.), for 6 hours, time afterwhich, 575 g of a clear reddish liquid are obtained, which contains therandom terpolymer derived from itaconic acid, aconitic acid or itsisomers and sodium vinyl sulfonate referred to as product 3, with andaverage molecular weight of 1061 AMU by number, an average molecularweight of 1220 AMU by weight and a polydispersity index of 1.15. Thesevalues were obtained by means of size exclusion chromatography (SEC)using a chromatography column with the trade name plaquagel MIXED-OH andan aqueous solution comprising sodium nitrate (0.2 M) and sodiumphosphate, monobasic (0.01 M) al a pH of 7 as the mobile phase.Spectroscopic characteristics are the following: FTIR (cm⁻¹): 3431,2939, 1713, 1407, 1154, 1036 y 715. ¹H NMR (D₂O), 200 MHz, δ (ppm):multiple signals at the 1.77 a 2.33, 2.72 a 3.02, 3.37 a 3.44. ¹³C NMR(D₂O), 50 MHz, δ (ppm): signals at the 23.2 a 31.5, 39.9 a 43.6, 49.1 a58.5 y 176.9 a 181.4 intervals.

3) Experimental evaluation of mineral salts scale inhibiting anddispersing properties of the random terpolymers. The assessment of theterpolymer anti-scaling and dispersant capabilities were performed bymeans of five different tests: a) Determination of calcium sulfate scaleinhibition, b) Determination of calcium sulfate and carbonate crystaldistortion and modification by scanning electron microscopy, c)Determination of calcium carbonate scale inhibition in a medium with thecharacteristics of cooling systems d) Determination of efficiency asinorganic salts dispersant, e) Determination of mineral scale inhibitionof calcium carbonate and calcium sulphates, barium and strontium, f)Determination of prevention and remediation of formation damage bycalcium sulphate precipitation with incompatible brine mixture in alimestone cores under high temperature, high pressure and high salinityconditions.

a) Determination of Calcium Sulfate Mineral Scale Inhibition. ForCalcium Sulfate.

The method consists in mixing two solutions to induce the formation ofcalcium sulfate.

1.—Two solutions are prepared containing the calcium and sulfate ions,respectively.

-   -   a) Solution containing calcium ions: it contains 7.5 gL⁻¹ of        NaCl and 11.1 gL⁻¹ of CaCl₂.2H₂O.    -   b) Solution containing sulfate ions: it contains 7.5 gL⁻¹ of        NaCl and 10.66 gL⁻¹ of NA₂SO₄.

2.—The desired inhibitor concentration is prepared in the solutioncontaining the sulphate ions.

3.—10 mL of each solution and the desired inhibitor concentration aremixed and everything is poured into a 25 mL hermetically sealed vial.

4.—The vials are placed in an oven for 24 hours at a constanttemperature of 70° C.

5.—After 24 hours, the vials are allowed to cool down to roomtemperature. Solids that may have been formed are filtered and a 1 mlsample is taken and completed to 10 ml with ultra-pure water.

6.—The solution is analyzed by means atomic absorption, in order toobtain the remaining concentration of calcium ions in the solution. Acontrol is prepared, containing only the amount of calcium ions presentin the blank. The inhibition percentage was estimated with theexpression (1).

$\begin{matrix}{{\%\mspace{14mu}{Inhibition}} = {\frac{\begin{matrix}{{Ca}_{{sample} - {after} - {the} - {precipitation} - {ion}}^{+ 2} -} \\{Ca}_{{Reference} - {after} - {the} - {lprecipitation}}^{+ 2}\end{matrix}}{{Ca}_{control}^{+ 2} - {Ca}_{{Reference} - {after} - {the} - {precipitation}}^{+ 2}}*100}} & (1)\end{matrix}$

Example 4

The determination of the calcium sulfate scale inhibitory capability wascarried out for product 1 and 3. Table 5 shown the results for product 1and 3 at different concentrations for products 1 and 3 and the derivedcopolymer from itaconic acid/sodium vinyl sulfonate (proportion 1:3).

TABLE 5 Calcium sulphate inhibition results Calcium concentrationEfficiency Product Concentration (ppm) (%) Control solution — 1509 —Reference — 1012 0 Producto 1 200 1495 97.2 400 1500 98.2 600 1504 98.9Producto 5 200 1493 96.8 400 1501 98.4 600 1503 98.8 Derived Copolymer200 1410 81.0 from itaconic acid/ 400 1425 83.1 sodium vinyl 600 143084.1 sulphonate (1:3 ratio)

A comparison of the results obtained with the terpolymers described asproducts 1 and 3, with the derived copolymer based on itaconicacid/sodium vinyl sulphonate in 1:3 ratio that it was described in theMexican Patent Application MX/a/2013/004644 which shown that newterpolymers have a better performance and that the chemical structure isa key element in the development of new anti-scaling agents withimproved properties. It is a key element in the development of newanti-scaling agents with improved properties.

c) Determination of calcium sulphate and carbonate crystals distortionor modification by scanning electron microscopy. The solutionscontaining the calcium and sulphate ions are the following:

-   -   i. Solution containing the calcium ions: it contains: 7.5 gL⁻¹        de NaCl and 21.32 gL⁻¹ of CaCl₂.2H₂O.    -   ii. Solution containing the sulphate ions: it contains: 7.5 gL⁻¹        de NaCl and 21.32 gL⁻¹ of Na₂SO₄.

1.—The desired inhibitor concentration is prepared in the solutioncontaining the sulphate ions.

2.—10 ml of each solution and the desired inhibitor concentration aremixed and everything is poured into a 25 mL hermetically sealed tube.

3.—The tubes are placed in an oven for 24 hours at a constanttemperature of 70° C.

4.—After 24 hours, the containers are allowed to cool down to roomtemperature without exceeding 2 hours. Subsequently the solids formedare filtered.

5.—Solids formed in the tubes are analyzed and their morphology isobserved by scanning electron microscopy (SEM).

Example 5

In order to determine the effect of the terpolymers derived from thepresent invention on calcium sulphate crystals, product 1 was evaluatedusing two brines with high concentrations of calcium and sulphate ions.

FIG. 4 shows the images and compositions of the crystals resulting fromthe mixture of the solution for:

-   -   a) without chemical product and b) with 200 ppm of product 1.        Noteworthy, it is possible to observe clearly how the product 1        breaks up and distorts the calcium sulphate crystals, thereby        inhibiting the growth of larger crystals.

For Calcium Carbonate

Solutions containing the calcium and bicarbonate ions are the following:

a) Solution containing the calcium ions: 12.15 gL⁻¹ CaCl₂.2H₂O, 3.68gL⁻¹MgCl₂.6H₂O and 33 gL⁻¹ de NaCl.

b) Solution containing the bicarbonate ions: 7.36 gL⁻¹ de NaHCO₃ and 33gL⁻¹ of NaCl.

2.—The desired inhibitor concentration is prepared in the solutioncontaining the bicarbonate ions.

3.—10 mL of each solution and the desired inhibitor concentration aremixed and everything is poured into a 25 mL hermetically sealed tube.

4.—The tubes are placed in an oven for 24 hours at a constanttemperature of 70° C.

5.—After 24 hours, the tubes are allowed to cool down to roomtemperature without exceeding 2 hours. Solids that may have formed arefiltered.

6.—Solids formed in the tubes are analyzed and their morphology isobserved by scanning electron microscopy (SEM).

Example 6

In order to determine the effect of the derived terpolymers from thepresent invention on calcium carbonate crystals, product 1 was evaluatedusing two brines with high concentrations of calcium and bicarbonateions.

FIG. 5 shows the images and compositions of the crystals resulting fromthe mixture of the solutions without chemical product and from themixture of the solutions with product 1, for: a) without chemicalproduct and at 200 ppm concentration of product 1.

It is possible to observe clearly how product 1 breaks up and distortsthe calcium carbonate crystals at the concentration of 200 ppm, therebyinhibiting the growth of the crystals. Furthermore, the chemicalcompound obtained by means of chemical analysis shows the presence ofsulfur in all solids, which confirms the presence of product 1 and hencethe formation of supramolecular complexes and their effect on thecalcium carbonate crystals morphology distortion.

c) Determination of Inhibition of the Characteristic Calcium CarbonateScale (CaCO3) of a Cooling System.

This method determines the efficiency of calcium carbonate salts scaleinhibitors.

Preparation of Solutions

Sodium carbonate solution (Na₂CO₃)

0.424 g of Na₂CO₃ is weighted in 1 L of demineralized water.

Calcium chloride solution (CaCl₂))

0.444 g of CaCl₂) is weighted in 1 L of demineralized water.

Preparation of Samples.

-   -   1. 100 mL of the Na₂CO₃ solution are poured in a 250 mL flask        with an air-tight cap.    -   2. The concentration to be evaluated is adden in mL (ppm).    -   3. 100 mL of the CaCl₂) solution are poured and the flask is        shaken.    -   4. A blank is prepared as in points 1 and 3 composed of Na₂CO₃        and CaCl₂) solutions without inhibitor and shaken.    -   5. All the flasks are closed and placed in the oven for 24 hours        at 70° C.    -   6. Once the testing time is completed, the flasks are removed        from the oven and left to cool down.    -   7. A reference solution without inhibitor composed of NaCO₃ and        CaCl₂) solutions is prepared as in points 1 and 3.    -   8. The amount of calcium ions in solution is determined for the        stock solution, for the blank and for the samples.

Table 6 shows a summary of the testing conditions.

TABLE 6 Testing conditions Calcium Hardness (CaCO₃) 200 ppm Temperature70° C. Test time 24 h Scale inhibitor concentration 5 and 10 ppm

Determination of Hardness as CaCO₃.

-   -   1. An aliquot is taken from the center of the sample bottle at        room temperature and at rest without having shaken since its        removal from the oven.    -   2. The amount of calcium ions is determined by titration with        EDTA (ethylenediaminetetraacetic acid disodic salt).

Efficiency Percentage Calculation:

${Efficiency}\text{:}\frac{{{sample}\mspace{14mu}{EDTA}\mspace{14mu}{mL}\mspace{14mu}{spent}} - {{blank}\mspace{14mu}{EDTA}\mspace{14mu}{mL}\mspace{14mu}{spent}}}{\begin{matrix}{{{Reference}\mspace{14mu}{solution}\mspace{14mu}{EDTA}\mspace{14mu}{mL}\mspace{14mu}{spent}} -} \\{{blank}\mspace{14mu}{EDTA}\mspace{14mu}{mL}\mspace{14mu}{spent}}\end{matrix}}*100$

Example 7

The determination of the inhibitory capability of calcium carbonatescale typical of cooling systems was carried out for products 1 and 2and for polymers commercially used as scale inhibitors. Following Table7 shows the efficiency results at different concentrations

TABLE 7 Efficiency results of polymers as scale inhibitors Efficiency atEfficiency Sample 5 ppm at 10 ppm Poly (acrylic acid) 63.8 81.6 Product1 93.5 95.1 Product 2 92.4 94.1

d) Determination of Efficiency as Inorganic Salts Dispersants

These methods consist in determining the performance of the synthesizedterpolymers to disperse calcium carbonate, iron oxides and clays throughthe measurement of turbidity in NTU (nephelometric turbidity units),where the dispersant action is more efficient at higher turbidityvalues. The measurement is founded on applying the nephelometrictechnique using a photometer (FIG. 6). The standard method is based onthe comparison of the amount of light dispersed by colloidal particlespresent in a water sample, with the intensity of the light emergingthrough the same sample. Turbidity is expressed in turbidity units(NTU), where a turbidity unit equals a formalin suspension in water witha concentration of 1 ppm. The measurements of turbidity allow evaluatingthe dispersant effect for the polymeric chains.

Calcium Carbonate Dispersion Evaluation

For this test, it was employed a brine with a hardness of 200 ppm ascalcium carbonate from sodium carbonate and calcium chlorides salts, and750 ppm reactive-degree calcium carbonate was added in order to measurethe effect of the terpolymer on calcium carbonate dispersion, at adispersant concentration of 10 ppm for a 2 hours as period time.

Example 8

The determination of the characteristic calcium carbonate dispersantcapability was carried out for the product 1. The dispersant effectresults for the product 1 of the present invention and for a commercialpolymer used as inorganic salts dispersants and their respectivemolecular weights are shown in Table 8. The results show that theproduct 1 work better at dispersing calcium carbonate than acrylic poly(acrylic acid).

TABLA 8 Turbidity results. Sample Turbidity (NTU) Poly (acrylic acid)23.5 Product 1 152.1

Iron Oxide Dispersion Assessment.

One of the problems that most affect aqueous systems is the presence ofiron oxides, due to the dissolution of metal by corrosion effects. Thismethod consists in evaluating the dispersant power of the synthesizedterpolymer as follows:

A solution is prepared with hardness as calcium carbonate of 200 ppm,750 ppm of iron oxide and with the dispersant product added. The mixtureis shaken and left to rest for a 4 hour time period. At the conclusionof the test, an aliquot is taken and turbidity is measured.

Example 9

The determination of the iron oxide-dispersant capability was carriedout for the product 1 at 25 ppm of concentration. The results of theiron oxide dispersion test by the product 1 of the present invention andby a commercial polymer used as inorganic salts dispersants and theirrespective molecular weights are shown in Table 9.

Table 9 results show that product 1 work better than the poly (acrylicacid).

TABLE 9 Turbidity results. Sample Turbidity (NTU) Poly (acrylic acid)345.2 Product 1 750.3

Clay Dispersion Assessment

For the purpose of this test, brine with a hardness of 200 ppm ascalcium carbonate and 1000 ppm of clay (kaolin) was prepared by puttingthese substances in contact and adding the dispersant, prepared at a 25ppm concentration.

Once mixed, the compounds is vigorously stirred in a magnetic stirringplate for 5 minutes and left to rest for 2 hours; once this time iselapsed, the respective turbidity measurements are performed.

Example 10

A determination of the clay-dispersing capability was carried out forthe product 1 at 25 ppm as concentration. The results of the clay(kaolin) dispersion test for the product 1 of the present invention andfor a commercial polymer used as inorganic salts dispersants are shownin Table 10.

TABLE 10 Results of turbidity. Sample Turbidity (NTU) Poly (acrylicacid) 550.6 Product 1 850.1

Table 10 results show that product 1 of the present invention performbetter at dispersing clays than the poly (acrylic acid) which iscommonly used as inorganic salts dispersants.

e) Determination of the Mineral Scale Inhibition of Calcium Carbonateand Calcium, Barium and Strontium Sulfates Scale Inhibition.

This evaluation involves the mixture preparation of 20 mL sea water andconnate water in a 3 to 1 ratio. The mixture water is heated at 70° C.for 8 hours and then observed whether or not crystals forming.

The product to evaluate is added into the sea water at the requiredconcentration.

Tables 11 and 12 show the brines compositions employed in thisexperiment.

The product to evaluate is added into the sea water at the requiredconcentration.

Tables 11 and 12 show the brines compositions employed in thisexperiment.

TABLE 11 Compositions of the brines Sea water Connate water Cations mgL⁻¹ mg L⁻¹ Sodium 11742 59809 Calcium 448 31880 Magnesium 1288 1944 Iron0.1 0.1 Barium — 25.37 Strontium 7.84 1450 Anions mg/L mg/L Chlorides19900 154000 Sulfates 3650 300 Carbonates 13 0 Bicarbonates 84 149

TABLE 12 Brines hardness and salinity Sea Water Connate Water (mg L⁻¹)(mg L⁻¹) Total hardness as CaCO₃ 6420 87700 Salinity as NaCl 32804253859

Example 11

The qualitative determination of calcium carbonate inhibition andcalcium sulfate, barium and strontium was made for the Product 1.

The results are shown in Table 13.

TABLE 13 Crystal Formation Reference High amount Product 1 No evidencie

Determination of Prevention and Remediation of Damage Caused by CalciumSulphate Precipitation with Incompatible Mixture of Brines in LimestoneCores at High Temperature and High Salinity Conditions

Prevention of damage by calcium sulphate precipitation in limestonecores at reservoir conditions.

The damage-prevention study was carried out using brines 1 and 2, thecomposition of which is shown in Table 14.

TABLE 14 Composition of the brines Brine 1 Brine 2 Cations mg/L mg/LSodium 2949 2949 Calcium 3020 — Anions mg/L mg/L Chlorides 4551  4551Sulphates — 10080

f) Procedure

-   1.—In a limestone saturated cores with brine 1 at 150° C. and 2000    psi, permeability was determined under such conditions.-   2.—Subsequently, brine 2 enriched with chemical product 1 from the    present invention was injected to the limestone cores saturated with    brine 1 in order for them come in contact and, afterwards,    permeability was measured under the temperature and pressure    conditions described in point 1.

Example 12

The damage remediation by precipitation of calcium sulfate in limestonecore at reservoir conditions.

Remediation of Damaged Caused by Calcium Sulphate Precipitation inCalcite Cores at Reservoir Conditions.

The damage-prevention study by calcium sulphate precipitation wascarried out at 150° C. and 2000 psi in an incompatible mixture brines(Brine 1 and 2) from the terpolymer described in Example 1 (product 1)according to this following procedure:

-   1.—In a calcite saturated core with brine 1 at 150° C. and 2000 psi,    permeability was determined under such conditions.-   2.—Subsequently, brine 2 was injected to the limestone cores    saturated with brine 1 in order for them come in contact and,    afterwards, permeability was measured under the temperature and    pressure conditions described in point 1.-   3.—Finally the brine 2 containing 200 ppm of product 1 was injected    to the calcite core and the permeability was measured.

Permeability at the beginning of the test with the limestone coresaturated with brine 1 yielded a result of 55 mD, and with the mixtureof brine 1 and 2 enriched with 200 ppm of product 1, permeability was 57mD.

This fact indicates that the injection of product 1 to the calcite corehad prevented the damage and even had an 3% increase in the initialpermeability.

Example 13

The effect of terpolymer described in Example 1 (product 1) wasdetermined in the prevention of damage caused by calcium sulfate incalcites cores at 150° C. and 2000 psi due to a mixture of incompatiblebrines and after to the product 1 injection.

The effect of terpolymer described in Example 1 (product 1) wasdetermined in the prevention of damage caused by calcium sulfate incalcites cores at 150° C. and 2000 psi due to a mixture of incompatiblebrines and after to the product 1 injection. The compositions of brineare shown in Table 14.

Permeability at the beginning of the test with the calcite coresaturated with brine 1 yielded a result of 58 mD, and with the mixtureof brine 1 and 2, permeability was 27 mD. This fact indicated that theincompatibility of brines generated a 47% reduction in permeability.

When brine 2 additivated with 200 ppm of the product 1, was injected,the permeability was 62 mD, so there was an increase of 6.9% compared tothe initial permeability (58 mD) system.

Assessment of acute toxicity with Daphnia magna and Artemia franciscana.This method is applicable to acute toxicity assessment in water andwater soluble substances. In fresh water bodies, industrial andmunicipal wastewater, agricultural runoff and pure or combinedsubstances or lixiviates and the solubilizable fraction in soils andsediments.

Within the cladocera group, the Daphnia gender species are the mostwidely used as bioindicators in toxicity tests, due to their widegeographic distribution, the important role they play within thezooplankton community, and because they are easy to culture in alaboratory and they are responsive to a wide range of toxics.

The acute toxicity determination was carried out by means of the MexicanNMX-AA-0087-SCFI-2010 standard, which establishes the method formeasuring acute toxicity, using the freshwater organism Daphnia magna(Crustacea-Cladocera) and the Artemia franciscana organism.

Example 14

The acute toxicity determination was carried out with Daphnia magna forproduct 1, using the testing procedure established and described in theNMX-AA-087-2010 standard. Table 15 shows the average toxicity result ofa total of three repetitions. The acute toxicity result indicates thatthe product 1 is in the category of not particularly toxic The resultindicates that acute toxicity of the product 1 is in the category ofparticularly not toxic for the organism Daphnia magna sweet aquaculture.

TABLE 15 Toxicity to Daphnia magna. Chemical product CL₅₀ (ppm)*Toxicity Category Product 1 102 Particularly Non-toxic 101 ParticularlyNon-toxic 100 Particularly Non-toxic Average 101 Particularly Non-toxic*Concentration range in ppm, classification^(a), category 5: 0.01-0.10,extremely toxic; 4: 0.1-1.0, highly toxic; 3: 1-10, moderately toxic; 2:10-100, slightly toxic; 1: 100-1000, particularly non-toxic and0: >1000, non-toxic. *CNS (UK) toxicity category for the application ofchemical products used in hydrocarbon production in the North Sea.

In addition to these facts, based on the NRF-005-PEMEX-2009 Mexicanstandard, where it is established that to use chemicals products in theoil industry it must meet the following environmental criteria.

For sweet environment for aquaculture, using daphnia magna the limit inunits of microorganism toxicity (UT), must not exceed 20 units. Thetoxicity units (UT) are calculated with CL50 value from the testtoxicity, from the following relationship:

UT=(1/CL ₅₀)×100

Where:

TU=Acute toxicity units

CL₅₀=Inhibitor concentration (in mgL−1 that causes the mortality of 50%of exposed organism).

Therefore, the terpolymer of the present invention has a TU=0.32, andhence it meets the Mexican NRF-005-PEMEX-2009 standard and can be usedin equipment and pipelines of oil and chemical industry that uses freshwater and is built in land

Example 15

The acute toxicity determination was carried out with Artemiafranciscana for product 1, using the test procedure established anddescribed in the NMX-AA-087-2010 standard. Table 16 shows the averagetoxicity result of a total of three repetitions.

TABLE 16 Toxicity to Artemia franciscana. Chemical product CE₅₀ (ppm)*Toxicity Category Product 1 220 Particularly Non-toxic 218 ParticularlyNon-toxic 221 Particularly Non-toxic Average 219.7 ParticularlyNon-toxic *Concentration range in ppm, classification^(a), category 5:0.01-0.10, extremely toxic; 4: 0.1-1.0, highly toxic; 3: 1-10,moderately toxic; 2: 10-100, slightly toxic; 1: 100-1000, particularlynon-toxicand 0: >1000, non-toxic. *CNS (UK) toxicity category for theapplication of chemical products used in hydrocarbon production in theNorth Sea.

The acute toxicity result indicates that product 1 is particularlynon-toxic to the Artemia franciscana organism. Moreover, based on theMexican NRF-005-PEMEX-2009 standard, which establishes that, in orderchemical products to be suitable for use in the oil industry, they mustmeet the following environmental criterion. For sea water environments,using the Artemia franciscana microorganism, the maximum limit intoxicity units should not be higher than 2.

Therefore, the terpolymer of the present invention has a TU=0.46, andhence it meets Mexican NRF-005-PEMEX.2009 standard and can be used inequipment and pipelines of oil and chemical industry that used sea wateror formation water from oil reservoirs and that is built offshore.

Determination of Acute Toxicity by Means of the Microtox Method.

The microtox bacterial bio-assay, designed by Strategic Diagnostic Inc.(Azur Environmental) is based on monitoring changes in the emissions ofnatural light by a luminescent bacteria, Vibrio fischeri (Photobacteriumphosphoreum).

The Microtox assay measures the acute toxicity of the test substancepresent in aqueous solution that uses a suspension of approximately onemillion of luminescent bacteria (Photobacterium phosphoreum) as testorganism. The suspension of micro-organisms is added to a series oftubes of dilutions at controlled temperature with differentconcentrations of the test substance, to subsequently read, in aphotometric device, the intensity of light emitted by each dilution,considering a reference blank where the test substance is not present.

With the obtained data, a dose-response graph can be drawn, by means ofwhich the CE₅₀ value is a measure of the decrease in the light emittedby the bioluminescent bacteria by means of the analyzing equipment, andspecifically represents the concentration at which a 50 percent decreaseof the light was obtained, with regard to a reference blank. Concretely,the CE₅₀ value indicates the relative toxicity of the test substance.

Example 16

The determination of acute toxicity was carried out with Vibrio fischeri(Photobacterium phosphoreum) for the product 1, using the test procedureestablished in the NMX-AA-112-1995-SCFI Mexican standard, used for theassessment of toxicity of natural and residual waters, as well as pureof combined substances, by means of the bio-luminescent bacteriaPhotobacterium phosphoreum. Table 17 shows the average toxicity resultof a total of three repetitions.

TABLE 17 CE₅₀ 15 min. (ppm) *Toxicity Category 21.8 Slightly toxic 21.6Slightly toxic 21.7 Slightly toxic

Toxicity results shown in Table 17 indicate that the derived product 1from the Example 1 is slightly toxic for Photobacterium phosphoreumbioluminescent bacteria.

1. A terpolymer, comprising:

wherein R₁=—H, —CH₃, R2=—H, —CH₂COOH, —COOH, R3=—COOH, R4=—CH2COOH, H,R5=—H, R6=—H, R7=—H, —CH3, R8=—SO₃Na, —CH₂SO₃Na, —CONHC(CH3)₂CH2S03Na,C₆H₄SO₃Na, Rg=H, R₁0=—COOH, R1₁=—COOH y R12=—CH₂COOH and n is between 2and 70, and wherein the terpolymer is derived from at least one ofitaconic acid or isomers, aconitic acid, or alkenylsuiphonates.
 2. Theterpolymer, according to claim 1, wherein the terpolymer is an activeagent for inhibiting and dispersing mineral scales of at least one ofcalcium carbonate, calcium sulphates, barium and strontium and disperseclays, calcium carbonate, calcium sulphates, barium and strontium andiron oxides.
 3. The terpolymer, according to claim 2, wherein theterpolymer inhibits and disperses mineral scales present in equipmentused in oilfields.
 4. The terpolymer, according to claim 1, wherein theterpolymer is administered at high pressure and ultra-high salinity. 5.The terpolymer, according to claim 1, wherein itaconic acid isomersinclude at least one of cis-glutaconic acid, trans-glutaconic acid,citraconic acid and mesaconic acid.
 6. The terpolymer according to claim1, wherein aconitic acid isomers include at least one of cis-aconiticacid and trans-aconitic acid.
 7. The terpolymer according to claim 1,wherein sodium alkyl sulphonates include at least one of vinyl sulfonicacid, allyl sulfonic add, styrene sulfonic add,2-acrylamido-2-methyl-1-propane sulfonic and salts thereof.
 8. Theterpolymer according to claim 5, wherein the salts include at least oneof sodium or potassium.
 9. The terpolymer, according to claim 1, whereinterpolymer chemical structure is a random-type structure.
 10. Theterpolymer, according to claim 1, wherein the average molecular weightby number is between about 500 AMU and about 31,000 AMU.
 11. A method ofinhibiting and dispersing carbonate and calcium sulfate mineral scale,comprising: adding a terpolymer to a cooling system or a boiler system,wherein the terpolymer, comprises:

wherein R₁=—H, —CH₃, R2=—H, —CH₂COOH, —COOH, R3=—COOH, R4=—CH2COOH, H,R5=—H, R6=—H, R7=—H, —CH₃, R8=—SO₃Na, —CH₂SO₃Na, —CONHC(CH₃)₂CH₂S0₃Na,C₆H₄SO₃Na, R9=H, R₁₀=—COOH, R₁₁=—COOH y R12=—CH₂COOH and n is between 2and
 70. 12. The method of claim 11, wherein the cooling system or theboiler system is used in the chemical or oil industry.
 13. The method ofclaim 11, wherein the method includes adjusting the temperature to anoperating temperature of up to about 220° C.
 14. The method of claim 11,wherein method includes adjusting the pressure to a pressure of up toabout 8000 psi.
 15. The method of claim 11, wherein the method includesa brine of salt.
 16. The method of claim 11, wherein in the brine salthas a concentration up to about 450,000 ppm.
 17. The method of claim 11,wherein in the brine of salt is calcium carbonate having a concentrationof about 250,000 ppm as a total hardness.
 18. The method of claim 11,wherein the concentration of the terpolymer is between about 1 to about10.000 ppm.
 19. The method of claim 11, wherein the terpolymer isdiluted in an aqueous medium.
 20. The method of claim 11, wherein theterpolymer meets the Mexican NRF-005-PEMEX-2009 standard for use in atleast one of equipment and pipelines that use fresh water and are builton land.
 21. The method of claim 11, wherein the equipment or thepipelines are used in at least one of a chemical or an oil industry. 22.The method of claim 11, wherein the terpolymer meets the MexicanNRF-005-PEMEX-2009 standard for use in off shore applications that usesea water or formation water from oil reservoirs.